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Method for the manufacture of thermoplastic panel heat exchangers

Assignee: DuPont Canada Inc
•
Filing: 1992-04-16
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Granted: 1993-03-23
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Expires: 2012-04-16
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Abstract

Abstract A method for the manufacture of panel heat exchangers from thermoplastic polyamides. At least one sheet is coated with a coating that facilitates bonding of the polymer to itself under the influence of heat. Two sheets, at least one of which has been coated, are placed between moulds in a press. At least one of the moulds has grooves corresponding to the pattern of fluid flow passages to provided in the panel heat exchanger. The moulds are heated and an inert gas e.g. nitrogen, is applied and passed through the fluid flow passages, to assist in the formation of the passages and to remove any voltatile material from the coating. The preferred coating is benzyl alcohol, phenol and polyamide. The heat exchangers may be used in a variety of end-uses, especially in automotive end-uses.

Inventors

  • 👤 Jerry P. Shuster
  • 👤 Anthony J. Cesaroni

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 18:47
CPC Classifications
F; F28; F28F; F28F21/00; F28F21/06; F28F21/065; B; B29; B29C; B29C49/00; B29C49/02; B29C49/06905; B29C49/0691; B29C51/00; B29C51/26; B29C51/266; B29C51/267; F24; F24S; F24S10/00; F24S10/50; F24S10/501; B29C65/00; B29C65/48; B29C66/00; B29C66/01; B29C66/05; B29C66/10; B29C66/11; B29C66/112; B29C66/1122; B29C66/40; B29C66/41; B29C66/43; B29C66/50; B29C66/51; B29C66/53; B29C66/534; B29C66/5346; B29C66/53461; B29C66/54; B29C66/70; B29C66/71; B29L; B29L2031/00; B29L2031/18; Y; Y02; Y02E; Y02E10/00; Y02E10/40; Y02E10/44; Y10; Y10T; Y10T29/00; Y10T29/49; Y10T29/4935; Y10T29/49366; Y10T29/49805

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 364 words
A method for the manufacture of a panel heat exchanger from a thermoplastic polyamide, said heat exchanger consisting essentially of first and second panels and inlet and outlet header means with said panels being bonded together to define fluid flow passages extending between the inlet and outlet header means, each of said panels being generally planar and formed from a sheet of said polyamide having a thickness of less than 0.7 mm, said panels having orifices therein cooperatively located at each of the inlet and outlet header means, each of said inlet and outlet header means being comprised of a distributor having planar ends, an axial flow passage and at least one radial flow passage, said method consisting essentially of the sequential steps of: (a) placing the two sheets of thermoplastic polyamide, at least one of which has been coated with a coating composition that will facilitate bonding of the sheets under the influence of heat, in face-to-face contact between moulds in a heated press, said coating being comprised of benzyl alcohol, each of said moulds being heated to a temperature in the range of 140°-200° C. and the surfaces of at least one of said moulds having a recessed pattern thereon corresponding to the fluid flow passages of the panel heat exchanger, such that (i) the sheets are in face-to-face contact with each other over substantially the entire face of the sheets and additionally in face-to-face contact with opposite ends of said distributors, the distributors being in a spaced apart relationship corresponding to the location thereof in the panel heat exchanger, and (ii) the coating is at the interface between the sheets; and (b) pressing said heated moulds to effect bonding between the sheets and between the sheets and the ends of the distributors and applying an inert gas between said inlet and outlet header means, said inert gas being applied for at least two cycles of (i) flushing the gas between the inlet and outlet header means and (ii) increasing the gas pressure to 1.3-2.75 MPa, thereby bonding said sheets together whilst forming fluid flow passages between the inlet and outlet header means and removing volatile matter from the fluid flow passages.
Claim 2
Independent Claim 364 words
A method for the manufacture of a panel heat exchanger from a thermoplastic polyamide, said heat exchanger consisting essentially of first and second panels and inlet and outlet header means with said panels being bonded together to define fluid flow passages extending between the inlet and outlet header means, each of said panels being generally planar and formed from a sheet of said polyamide having a thickness of less than 0.7 mm, said panels having orifices therein cooperatively located at each of the inlet and outlet header means, each of said inlet and outlet header means being comprised of a distributor having planar ends, an axial flow passage and at least one radial flow passage, said method consisting essentially of the sequential steps of: (a) placing the two sheets of thermoplastic polyamide, at least one of which has been coated with a coating composition that will facilitate bonding of the sheets under the influence of heat, in face-to-face contact between moulds in a heated press, said coating being comprised of benzyl alcohol, each of said moulds being heated to a temperature in the range of 140°-200° C. and the surfaces of at least one of said moulds having a recessed pattern thereon corresponding to the fluid flow passages of the panel heat exchanger, such that (i) the sheets are in face-to-face contact with each other over substantially the entire face of the sheets and additionally in face-to-face contact with opposite ends of said distributors, the distributors being in a spaced apart relationship corresponding to the location thereof in the panel heat exchanger, and (ii) the coating is at the interface between the sheets; and (b) pressing said heated moulds to effect bonding between the sheets and between the sheets and the ends of the distributors and applying an inert gas between said inlet and outlet header means, said inert gas being applied for at least two cycles of (i) flushing the gas between the inlet and outlet header means and (ii) increasing the gas pressure to 1.3-2.75 MPa, thereby bonding said sheets together whilst forming fluid flow passages between the inlet and outlet header means and removing volatile matter from the fluid flow passages.
Claim 3
Dependent Claim 19 words
The method of claim 1 in which the coating composition is also applied to the ends of the distributors.
Claim 4
Dependent Claim 15 words
The method of claim 1 in which the distributors have at least two radial orifices.
Claim 5
Dependent Claim 11 words
The method of claim 1 in which the gas is nitrogen.
Claim 6
Dependent Claim 12 words
The method of claim 1 in which the polyamide is polyhexamethylene adipamide.
Claim 7
Dependent Claim 19 words
The method of claim 5 in which the temperature of said mould is in the range of 150°-180° C.
Claim 8
Dependent Claim 19 words
The method of claim 6 in which the pressure of inert gas is in the range of 1.5-2.5 MPa.
Claim 9
Dependent Claim 25 words
The method of claim 1 in which the panel heat exchanger has linear fluid flow passages with a width in the range of 1.2-2.5 mm.
Claim 10
Dependent Claim 19 words
The method of claim 1 in which the coating composition is an admixture of benzyl alcohol, phenol and methanol.
Claim 11
Dependent Claim 14 words
The method of claim 1 in which the gas is applied for 4-6 cycles.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1996-03-22 1996-09-21 1997-03-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2000-03-22 2000-09-21 2001-03-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2004-03-22 2004-09-21 2005-03-23 $7700.00 Window Closed / Lapsed

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